1. Find the pressure difference across a damper in an air duct. The fluid in the manometer has a RD of 1.09 and there is a height difference across the manometer's fluid of 2.25 cm.
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- The density of water is 1.00 × 10³ kg/m³, and the density of mercury is 1.36 × 10¹ kg/m³. Calculate the absolute pressure på at the bottom of a 0.250-m tall graduated cylinder that is one-fourth full of mercury and three-fourths full of water. Pb = PaWater moves through a constricted pipe in steady, ideal flow. At the lower point shown in the figure below, the pressure is 1.65 ✕ 105 Pa and the pipe radius is 2.60 cm. At the higher point located at y = 2.50 m, the pressure is 1.29 ✕ 105 Pa and the pipe radius is 1.40 cm. a) Find the speed of flow in the lower section. b) Find the speed of flow in the upper section. c) Find the volume flow rate through the pipe.Please asap
- 78. A pipe is horizontal and carries oil that has a viscosity of 0.14 Pa ?s.The volume fl ow rate of the oil is 5.3 3 1025 m3 /s. The length of the pipe is37 m, and its radius is 0.60 cm. At the output end of the pipe the pressureis atmospheric pressure. What is the absolute pressure at the input end?3. Water moves through a constricted pipe in steady and ideal flow. At the lower point shown in figure, the pressure is 1.75 × 105 Pa and the pipe radius is 3.00 cm. At the higher point located at y = 2.50 m, the pressure is 1.20 x 105 Pa and the pipe radius is 1.50 cm. Find the speed of flow (a) in the lower section and (b) in the section. upper P2 P1 Address 99+ PrtScn Home End4.0 mm 16. Consider the following diagram. (let air be an ideal, incompressible fluid) 2.0 cm 1200 cm'/s a. If the air is found to have a flow rate of 1200 cm3/s as it leaves the 4.00 mm diameter pipe, what is the velocity of the air in both segments of the pipe? b. If the density of air is 1.28 kg/m3 and the end of the pipe on the right opens up to the atmosphere, what is the pressure of the pipe at the 2.00 cm diameter section? C. If the fluid in the bottom of the U-tube is mercury with a density of 13,600 kg/m3 what is the difference between the surface levels of both sides of the tube, marked as h in the diagram?